US7558634B2 - Controller and method of controlling an apparatus using predictive filters - Google Patents
Controller and method of controlling an apparatus using predictive filters Download PDFInfo
- Publication number
- US7558634B2 US7558634B2 US11/513,681 US51368106A US7558634B2 US 7558634 B2 US7558634 B2 US 7558634B2 US 51368106 A US51368106 A US 51368106A US 7558634 B2 US7558634 B2 US 7558634B2
- Authority
- US
- United States
- Prior art keywords
- signal
- circuitry
- controller
- control signal
- disturbance
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime, expires
Links
Images
Classifications
-
- G—PHYSICS
- G05—CONTROLLING; REGULATING
- G05B—CONTROL OR REGULATING SYSTEMS IN GENERAL; FUNCTIONAL ELEMENTS OF SUCH SYSTEMS; MONITORING OR TESTING ARRANGEMENTS FOR SUCH SYSTEMS OR ELEMENTS
- G05B13/00—Adaptive control systems, i.e. systems automatically adjusting themselves to have a performance which is optimum according to some preassigned criterion
- G05B13/02—Adaptive control systems, i.e. systems automatically adjusting themselves to have a performance which is optimum according to some preassigned criterion electric
- G05B13/0265—Adaptive control systems, i.e. systems automatically adjusting themselves to have a performance which is optimum according to some preassigned criterion electric the criterion being a learning criterion
Definitions
- This invention relates to control methods and apparatuses, and in particular to electronic or computerised control apparatuses incorporating predictive electronic filters.
- control system Many types of control system are known and implemented in all manner of consumer and industrial machines and in industrial processes. These control systems are invariably based on a closed loop in which a control variable is sensed, compared with a desired or set value to derive an error signal, and a correlation applied in response to the error signal, hopefully to drive the error to zero.
- the stability of the control system is paramount, however, and filter functions are included in the feedback paths implicitly or explicitly to maintain stability.
- filter functions are included in the feedback paths implicitly or explicitly to maintain stability.
- additional feedback and “feed-forward” mechanisms have evolved to improve the performance of control systems, particularly in their speed of response.
- the need for stability limits these approaches in a well-known manner, particularly when filter functions have to be calculated and implemented allowing for variations and tolerances in a range of conditions.
- Predictive adaptive filters are also known and exploit the fact that a signal is usually changing slowly compared to the change of the additive noise. This is due to noise comprising all frequencies, while signals comprise predominantly low frequencies. Initially such an adaptive filter has a pre-defined setting but this setting will then continuously adapt to the changing signal, seeking to eliminate the noise in an optimal manner. This is achieved by comparing the momentarily arriving signal to the signal of the immediate past by means of an intrinsically built in mechanism, which can be pictured as an auto-correlation. Such filters react to changes in the signal to adapt the filter settings accordingly. As a consequence such filters are able to predict (extrapolate) the shape of the input signal for the immediate future, with decreasing prediction reliability for increasing temporal (predictive) intervals.
- Kalman-type filters which are able to adapt to the characteristics of an input signal using recursive estimation. By such an adaptation mechanism these filters remain optimally tuned to their respective task. Due to the extent to which analogue electronic signals are disturbed by noise, such predictive adaptive filters have a broad application domain in all fields of analogue electronic signal processing, for example, telecommunication, broadcasting, radar signal processing and many more. These filters, however, rely on the self-similarity of the input signal (that is, they are optimised to respond to particular characteristics of the expected signal). Their aim is to preserve a maximum amount of information from the input signal. Thus, the output signal is usually only an improved version of the original signal derived directly from the input. Accordingly, the Kalman filter, although interesting in itself, does not offer a solution to the problems of complex, control systems.
- the invention provides a controller for controlling a physical apparatus, the controller comprising first input means for receiving a primary input signal representing a measured state of the apparatus, and signal processing means responsive to said primary input signal for generating a control signal for influencing the state of the apparatus so as to maintain a desired state, the controller having at least one further input for a signal representing additional measurements of the apparatus or its environment, said signal processing means including correcting means for including corrections in said control signal in response to said additional measurement signal, and means for conditioning the response of said correcting means automatically in response to temporal cross-correlation observed between said additional measurement signal and said control signal observed during operation of the controller and apparatus together.
- the conditioning means may comprise means for adjusting a gain and frequency response of a signal path in the correcting means. Such an adjustment is similar to that implemented in a Kalman filter.
- the correcting means comprises means for filtering the additional signal via a plurality of filters having different fixed impulse responses and means for forming a weighted sum of the differently filtered signals to derive the correction to be applied, the conditioning means comprising means for adjusting the weightings of the different signal paths in response to their respective observed correlation with the control signal.
- the inventors refer to the correcting and conditioning means in this case as a cross-modal predictive filter (CMP filter).
- CMP filter cross-modal predictive filter
- the correcting and conditioning means in this case also has similarities with the well-known “neural network” circuits, in which cross-correlation between desired outputs and a set of inputs is learned from a number of sample patterns.
- the individual input signals coming from respective sensors as in the neural network they are in this case signals from the same sensor, but subject to different filter responses.
- the novel controller effectively learns the temporal correlation between the additional measurement signal and the control signal.
- the conditioning means may be arranged to observe said correlation by multiplying the signal of each path with a derivative of the control signal and integrate the product of said signals over time to derive said weighting.
- the integration may be lossy or not lossy, depending on the whether the conditioning is to be held forever in the absence of stimulation, or is to be allowed to decay.
- the integration does not need to be lossy in order for the CMP filter to be capable of adapting to temporal changes in the disturbances.
- the controller may have plural additional inputs, each with associated correcting means and conditioning means within the signal processing means.
- the correcting means for each additional signal need not all have the same number of filters, nor the same set of impulse responses. The number of filter paths can thus be reduced if the designer has some idea of the range of correlation expected.
- the controller may be arranged to generate plural control signals based on at least some of the same input signals, the signal processing means including correcting means and conditioning means for generation of each control signal.
- the plural correcting means may share filter components.
- a first control signal may be connected to serve as an additional measurement input to the correcting means for generating a second control signal.
- a derivative or other transformation may be applied to any of the measurement inputs, as appropriate to the application.
- the invention further provides a method of controlling a physical apparatus, the method comprising on a continuous basis:
- the correcting step may comprise filtering the additional signal via a plurality of filter functions having different fixed impulse responses, and forming a weighted sum of the differently filtered signals to derive the correction to be applied, the conditioning step comprising adjusting the weightings of the different signal paths in response to their respective observed correlation with the control signal.
- the conditioning step may begin from a zero condition, or may begin with a set of conditions learned in another apparatus.
- the invention further provides a controller of the type set forth above, wherein the correcting means is replaced by one having a fixed response, but one which has been transferred from another controller which has learned the response in operation. Whether this is practical will depend on the repeatability of the environment and the characteristics of the apparatus under control.
- a further alternative is to transfer learning from one controller into another controller as a starting condition, the other controller then being able to adjust the response of the correcting means during its continuing operation.
- FIG. 1 is a generalised block diagram of a conventional chemical processing plant, showing a typical closed loop control system
- FIG. 2 shows schematically the values of certain signals over time in a typical closed loop control system responding in a reactive manner to an external disturbance
- FIG. 3 shows the chemical processing plant of FIG. 1 modified with a CMP filter-based controller performing closed loop control of the steam entering the plant based on both the input and the output parameters of the plant;
- FIG. 4 shows the signals corresponding to those in FIG. 2 , in a closed loop control system using a cross-modal predictive filter responding directly to the same external disturbance after a learning phase;
- FIG. 5 is a schematic block diagram of a generalised process control system incorporating a CMP-filter based controller according to a generalised embodiment of the present invention
- FIG. 6 shows in more detail a multi-stage CMP filter within the control system of FIG. 5 ;
- FIG. 7 shows response curves of a set of resonators in a CMP filter of the type shown in FIG. 6 , when presented with a square pulse stimulus;
- FIG. 8 shows in more detail a gain control circuit (GCC) associated with each resonator in the CMP filter of FIG. 6 ;
- GCC gain control circuit
- FIG. 9 shows relationship between a single resonator output signal u.sub.i, a control signal v driving the process and its derivative v 1 , with respect to time;
- FIG. 10 is a schematic block diagram of an alternative form of CMP filter in which each resonator has a variable frequency response
- FIG. 11 is a schematic block circuit diagram for a robot control system forming a more specific embodiment of the present invention.
- FIG. 12 is a simulation of the path of the robot under control of the circuit of FIG. 11 as it encounters obstacles in an environment over a period of time;
- FIG. 13 illustrates the learning of optimum resonator weights for one disturbance signal within the robot circuit during the time period represented in FIG. 12 .
- This invention is not specifically limited to embodiment in either analogue or digital hardware, or software.
- the following description is generally valid for either implementation, special differences being pointed out as required.
- the mixture of analogue and digital circuits, and of hardware and software, which is used in a given application will depend on many factors familiar to the skilled person. Such factors include the bandwidth required for the system, the relative development costs of the different solutions, and the expected scale of production.
- actuator position is measured by a position-sensor, the signal from which is used by way of closed loop control to compensate for the internal forces that determine the mechanical motion pattern of the actuator. If an external force (disturbance) upsets the position, the control generates a signal to compensate.
- the combined inertia of the actuator and controller induces a time lag in the compensation used to counteract that disturbance, resulting in a significant position error during the compensation (transition) period.
- FIG. 1 represents a typical process 102 transforming a starting substance I into a product P by means of heat-controlled reaction.
- the starting substance normally enters the process with temperature T 1 .
- the optimal output is reached at T 2 .
- the complete plant 100 comprises control systems for maintaining the various parameters at their optimum levels to ensure process stability. Temperatures T 2 is fed back as signal FB and used as the set point in a conventional closed loop controller to control the flow rate 104 via valve 106 of the steam S that heats the plant.
- the output temperature T 2 will change if T 1 is fluctuating due to a disturbance, which will lead to a sub-optimal situation.
- FIG. 2 provides a graph showing schematically values of demanded, actual and error values (T.sub.D, T 2 and Err respectively) during the transition period of the chemical process closed loop control system, following a step change (disturbance) in the input temperature T 1 .
- T.sub.D represents the set or demand value for T 2 .
- some of the process parameters will be at their non-optimum settings, impacting the quality of the heat controlled reaction and its resultant output.
- FIG. 3 shows a modified control system in which a controller 200 receives not only the output signal T 2 , but also receives the “disturbance” signal T 1 .
- the exact causal relationship between variations in T 1 and the output signal T 2 is unknown, when the system is designed and set up.
- the novel controller 200 learns by an adaptive process to correlate an initially unknown change in T 1 (disturbance) with the delayed change in T 2 . The exact implementation of this is not described here, but is described below with reference to FIGS. 5 to 10 .
- valve 106 will be adjusted by signal FB to alter the flow rate FR to a pre-compensating setting.
- the plant 100 will be capable of responding directly to the disturbance in T 1 , anticipating the resultant effect on T 2 and consequently the error in T 2 (and its negative effect upon the process) will be greatly diminished, as shown in FIG. 4 .
- the novel type of controller can be designed to compare any number of different input signals and, by an adaptive process, learn to predict the output by observing the cross-correlation properties between the inputs and the output signal.
- the controller in particular can learn from its observations which of the numerous input signals is relevant to prediction of the output signal, and in what way.
- Embodiments of the invention include a cross-modal predictive (CMP) filter built into the control loop, which receives multiple inputs. After a learning period, the CMP filter will predict an output event (output signal) by responding to the earliest occurring relevant input that consistently precedes the related output signal.
- CMP cross-modal predictive
- the CMP filter would measure the external forces (disturbances) and—during the adaptive process—temporally correlate them to the (much later occurring) position change. Once the filter has adapted to the disturbances a position correction signal (a counter force) can be generated as soon as an external force occurs, without having to wait until a lagging position-error is detected at the output. Thus, the system will be capable of responding immediately to the application of an external force and the position error will be greatly diminished.
- FIG. 5 shows a CMP filter-based controller 200 in a typical closed-loop configuration, that is, with an output demand value v fed into and adjusting the operational setting of the controlled apparatus, here represented by generalised plant 100 .
- a reference signal P representing the current actual state of plant 100 is subtracted 202 from a desired (set) value SV (which can be zero), to provide a difference or error term x R , which is fed back into the controller, where it is used to define the output demand value, thereby “closing” the control loop.
- a number of external disturbance inputs x 1 . . . x N are also fed into the controller. These are derived from sensors throughout the plant 100 and comprise voltage time-functions of arbitrary shape.
- the plant 100 has to be specified according to the actual application domain, for example a force-position transformation as described in the earlier mechanical example, or a steam-heating device as described in the earlier chemical processing plant example.
- a force-position transformation as described in the earlier mechanical example
- a steam-heating device as described in the earlier chemical processing plant example.
- the skilled person will readily appreciate that the principles of the novel controller are applicable in a wide range of “physical” apparatuses and systems, from classic machines to economic systems.
- FIG. 6 shows a process control system using a very simple CMP-filter based controller in addition to conventional error signal x R .
- Plant 600 is shown emitting the conventional result signal P, and also two disturbances x 1 , x 2 .
- the number of disturbances is not restricted to two. Although these are shown coming from the plant in its broadest sense, they are for the purpose of conventional control systems environmental measurements, whose influence on the process is not exactly known.
- Subtraction circuit 602 receives the set value signal SV and derives the conventional error signal x R .
- This path 600 , 602 , 604 forms the standard proportional term reference loop of a closed loop control system, and warrants no further description.
- the summing circuit 606 permits many additional contributions to determine the control value v jointly with the conventional term besides u R , each from a disturbance “channel” responsive to one of the disturbance signals x 1 , x 2 etc.
- Each disturbance channel comprises a resonator 611 - 615 with fixed transfer function h i (fixed impulse response), generating a respective filtered signal u i accordingly.
- Each signal n i passes through a variable gain block 621 - 625 with gain ⁇ i to define the (positive or negative) strength of contribution of that channel in the summing circuit 606 .
- Resonators 611 - 615 are of a form well known per se, and comprise band-pass filters, which can be implemented in analogue, circuitry as LRC-circuits (inductor, resistor, capacitor) or in digital circuitry as IIR (Infinite Impulse Response) or FIR (Finite Impulse Response) filters.
- Each input disturbance x i is processed by at least one resonator channel.
- the number of channels associated with each disturbance signal is not fixed, and is determined by the known shape of the input waveform and the desired response by the controller to it. In the example illustrated, signal x 1 feeds M channels, while signal x 2 feeds N channels.
- Completing the CMP filter section of the controller shown in FIG. 6 are a differentiator 630 , which receives the control output signal v, and individual gain control circuits (GCCs) 631 - 635 , each controlling the gain of a respective gain block 621 - 625 .
- GCCs 631 - 635 provide the learning mechanism of the CMP filter, and will be described in more detail below, with reference to FIG. 8 .
- FIG. 7 shows how the resonator responses (u 0 , u 1 , u 2 etc.) differ, using the example of a square pulse function as input x.
- the characteristics of its associated resonator 611 etc. are chosen to provide a unique response to each input disturbance.
- Their resonant frequencies might progress logarithmically (for example f 0 , f 0 /2, f 0 /4 etc.).
- FIG. 8 shows in more detail one of the gain control circuits 631 - 635 which, together, provide the “learning” mechanism of the controller.
- Each unit 631 - 635 in this embodiment provides a multiplier function 800 and an integrator function 802 .
- Differentiator 630 shown again here for clarity, provides the derivative v′ of the control variable v as it is continuously output by summing circuit 606 .
- the derivative term provides a 90° phase-advanced version of the control signal, and can be regarded theoretically as a predictor of that signal.
- Differentiator 630 can be implemented using well known technology in analogue form by a differentiator or digitally by subtracting successive samples of the signal, or by a more sophisticated FIR or IIR filter function.
- Multiplier 800 multiplies together the resonator output u i , a damping factor ⁇ (typically a small fraction, to avoid instability) and the derivative term v′ to derive a measure of the correlation between the resonator output and the derivative v′.
- This correlation measure ⁇ i is produced continuously (either as an analogue signal or in a digital system as a stream of discrete sample values) and is integrated over time by integrator function 802 to adjust the actual gain ⁇ i of the respective gain block 621 - 625 etc.
- the integrator function would comprise a simple numerical accumulator.
- the components hereto described provide a controller that (during operation in a new environment) “learns” the relationship between input disturbances and their effect on the process, such that the response by the process to disturbances can be predicted and compensated for in an anticipatory manner, rather than a purely reactive manner.
- the operation of the CMP filter can be described by the following mathematical equations.
- u is given by:
- u 1 ( t ) z 1 ( t ) h 1 ( t ) (2)
- x is convolved with h.
- functions h are the transfer functions of resonators 611 etc given by:
- f the resonant frequency of the relevant resonators 611 - 615 and Q is their damping factor.
- Q is approximately identical to the number of oscillations a resonator will make in response to a ⁇ -function input.
- Q would preferably be approximately 1, for example lying in the range 0.5-1.2.
- the frequency response depends upon the reaction time required of the controller in a real application.
- f can be very high (kilohertz to megahertz), if used in a mechanical system f will normally be in the 1-100 hertz range, if used in chemical control situations f can be in the range of millihertz or even lower.
- the process of changing the gains associated with each disturbance term x i is a process of adaptation by a simple variety of neural learning.
- Each gain setting of the variable gain blocks 621 - 625 is modified by its respective gain control circuit (GCC) 631 - 635 . All gain control circuits 631 - 635 are identical (but receive different inputs).
- ⁇ is a small number typically in the range of 0.000001 to 0.1, which is a damping factor applied to all variable gain blocks 621 - 625 to prevent too rapid gain changes
- v′(t) is the temporal derivative of v(t) computed by the differentiator 630 , which produces a signal in direct proportion and polarity to the rate of change of its input signal.
- FIG. 9 provides waveforms showing the relationship between v, v′ and u i in a case where the particular function u i is well correlated with a peak in the derivative v′.
- the differentiator operates on only the one term v, it does not need to be ‘physically’ present in each gain control circuit 631 - 635 , and can exist as a common device 630 as shown in FIG. 6 , feeding one result into all channel gain control circuits 631 - 635 .
- the derivative function may be implicit somewhere in the control system already, and an explicit step would be omitted.
- the learning process in a CMP filter based closed-loop control system is a convergent process that will stop by itself (which prevents infinite growth of the gains ⁇ ), settling at the optimum values for the various disturbances.
- the reason for this is that during the process of adaptation to one or more disturbances x i , the process control variable will adjust to counteract the disturbances x i , and, thus their relative effect will gradually diminish. As a consequence the effect of the disturbances x i is gradually removed from the process and the gain value(s) ⁇ i for each particular disturbance response u i will settle at its optimum value. Adaptation will continue when a change occurs in a disturbance that is not fully compensated for by the current setting of its associated gain value.
- the damping factor ⁇ (which need not be the same for each disturbance) effectively sets the number of coincidences that have to be observed in order to constitute a definite correlation.
- FIG. 10 shows a block diagram of a modified CMP filter, whereby in place of multiple fixed resonators, one or more Resonator Response Control Circuits (RRCC) 1000 adjust for disturbance x 1 the frequency responses within variable-response resonators 1010 , 1020 . Primarily this will involve adjusting the resonant frequency, but in principle the Q factor could also be adjusted.
- the disturbance channel for disturbance x 2 comprising variable resonators, variable gain blocks 623 to 625 and gain control circuits 633 to 635 are not shown in this detail.
- the rest of the components of the CMP filter shown in FIG. 10 such as conventional block 604 , summation device 606 and differentiator 630 , can operate in the same manner as for the CMP filter of FIG. 6 and therefore warrant no further description.
- variable-response resonators 1010 , 1020 provides the advantage of reducing the number of resonators required to correlate disturbances x 1 with the process control term v. Instead of requiring a large quantity of resonators, such as ten, per disturbance the same effect can be achieved using preferably no more than two variable response resonators per disturbance, a disadvantage being that, in addition to increased circuit complexity, the learning process is slightly extended as the variable resonators also have to adjust to match the disturbances. Care must also be taken to preserve control loop stability.
- Each Resonator Response Control Circuit (RRCC) 1000 works in the following manner.
- An indicator of the correlation success for each disturbance is the magnitude of the weight terms from each Gain Control Circuit (GCC) 631 , 632 . These are used, in co-operation with the output from each channel's resonator u i and the derivative of the process term v′, to modify the frequency response of each variable-response resonator 1010 , 1020 in order to maximise the magnitude of the weight terms at the optimum correlation of disturbance to process term v. If more than one variable-response resonator 1010 , 1020 is being used per disturbance signal x 1 , as shown in the example of FIG.
- the RRCC ( 1000 ) assesses all relevant signals associated with the disturbance to adjust the frequency response of all of the resonators associated with that particular disturbance. Different responses will be chosen for the resonators associated with each disturbance to maximise the correlation windows during the initial periods of learning, with the windows narrowing as learning progresses and optimum settings are achieved.
- FIG. 11 presents a practical example of a controller for a moving robot 1100 , in order to demonstrate the functionality of this invention.
- the robot employs bump sensors 1102 (FL, 1102 (FR), 1102 (BL), 1102 (BR), one on each corner, and three visual range sensors, one forward-looking sensor, 1104 (F) and the other two front corner looking sensors 1106 (FL), 1106 (FR).
- Sensor suffixes L, R, F, B used individually or in combination, respectively denote “left”, “right”, “front” and “back”.
- a more complex CMP filter-based controller is adopted in the robot control system, whereupon there are two closed loop control systems ( ⁇ ), (s), that do not operate in isolation, but are closely coupled to one another.
- ⁇ closed loop control systems
- the control system comprises similar components as for previous examples: for each visual (range) disturbance there are corresponding banks of resonators 1108 etc. (in this particular example they are fixed response, but could be variable-response using fewer weights), for each physical (bump) disturbance there are corresponding fixed-response filters 1110 (L), 1110 (R), 1110 (F), 1110 (B), Gain Control Circuits 1112 ( ⁇ ), 1112 (s) etc. and summation devices 1114 ( ⁇ ), 1114 (s).
- the controller also comprises an additional derivative block f′ 1116 and a biasing means 1118 , the operation of which is described later.
- Bandpass filters 1110 (L), 1110 (R), 1110 (F), 1110 (B), are analogous to the fixed-response blocks 604 of FIG. 6 processing x R .
- Resonators 1108 etc., GCCs 1112 ( ⁇ ), 1112 (s) etc. and the gain blocks are analogous to the resonators 611 etc., GCCs 631 etc. and variable gain blocks 621 etc. of FIG. 6 processing disturbance signals x 1 ,X 2 , etc.
- Three representative channels with responses f, f/ 2 , f/N are shown for each disturbance.
- circuit could be implemented entirely in digital form or entirely in analogue form, in any mix of these, and in any mixture of hardware and software, as appropriate.
- the robot 1100 will initially use its bump sensors 1102 to inform the control system of the boundaries in which it is operating, using reverse and steering to negotiate past each obstacle.
- the visual range sensors 1104 (F), 1106 (FL), 1106 (FR) potentially inform the control system of an imminent collision, but the control system initially will not have learnt the association between the visual stimuli and a bump signal that occurs temporally slightly later.
- the robot closed loop control system will be capable of modifying the control paths associated with traction s and especially steering ⁇ by the direct influence of the visual sensors 1104 (F), 1106 (FL), 1106 (FR), steering the robot 1100 away from an obstacle before it hits it.
- each bump sensor 1102 (FL), 1102 (FR), 1102 (BL), 1102 (BR), is fed into both control loops.
- the front bump sensors 1102 (FL), 1102 (FR) are coupled together as a negative signal into the speed (s) control loop for reverse speed control and the back bump sensors 1102 (BL), 1102 (BR) are coupled together as a positive signal into the speed (s) control loop for forward speed control.
- An additional biasing means 1118 is fed into the same speed (s) control loop to set a non-zero speed so that an unstimulated robot moves at a constant forward speed until it receives a signal from an environment sensor 1102 (FL), 1102 (FR), 1102 (BL), 1102 (BR), 1104 (F), 1106 (FL), 1106 (FR).
- the right-hand side bump sensors 1102 (FR), 1102 (BR) are coupled together as a negative signal into the steering ( ⁇ ) control loop for left direction control and the left-hand side bump sensors 1102 (FL), 1102 (BL) are coupled together as a positive signal into the steering ( ⁇ ) control loop for right direction control.
- An unstimulated robot will move straight-ahead until it receives a signal from an environment sensor. It will be appreciated that a robot having a real job to do will be given additional stimuli to indicate desired changes in speed and direction, which will influence the controller in combination with the sensor inputs illustrated here.
- the resonators for the bump sensor signals are given a relatively low Q, such as 0.6, to provide high damping and avoid “overshoot” in their response (after a bump the robot should reverse, and not oscillate back and forward).
- the forward, left and right looking range sensors 1104 (F), 1106 (FL), 1106 (FR) are fed into their own dedicated banks of resonators 1108 whose outputs feed into both control loops s, ⁇ .
- control loop cross-coupling is achieved by taking each output control variable s and ⁇ (from the summation devices) and feeding it respectively into a bank of resonators feeding into the other control loop.
- the speed control influencing the steering ( ⁇ ) control its derivative f′ is first taken to remove the offset from the speed constant bias 1112 . Without control loop cross-coupling the CMP filter would not be able to relate a change in speed with a change in direction and a change in direction with a change in speed.
- the visual sensors will always be able to steer the robot away from obstacles, and the bump sensors would therefore never be activated, but in reality the robot will still have the potential to get into situations that it cannot steer out of.
- the bump sensors 1102 will still be required, but more as a secondary sensor, rather than the primary sensor they were at the beginning of the learning process.
- Some typical situations might be driving into a darkened dead-end passage, or when reversing and hitting an obstacle (there are no reversing visual sensors in this example, although the skilled reader will appreciate that this could be achieved with the addition of further sensor and control terms).
- the present invention only needs to be configured with control loop parameters that ensure that the control of the robot is smooth, such as resonator responses that are tailored to the visual sensor outputs. None of the parameters are environmental, but associated with the design of the robot. They are only set at the point of design of the robot and need no further adjustment. In contrast, a traditional robot would need to be taught new parameters associated with every new environment in which it has to operate.
- the novel controller would allow a robot to be placed in differing environments without needing any adjustment, and also adapts its response as the mechanism of the robot wears, or the nature of the environment changes.
- the robot (simulated here on a computer) traversing a “maze” full of obstacles, starting at point “0” and finishing at ‘11000’ (time steps, of arbitrary value).
- the CMP filters adjust to provide a relationship between visual sensing, steering and speed.
- the number of collisions gradually reduces, to the point that the robot manages to traverse long distances without any collisions, in particular from the top-left corner (time steps 7900 - 8900 ) to the end point.
- Small steering corrections can be seen where the visual sensor has indicated an impending collision, causing the steering loop to adjust in advance, steering the robot away from the obstacle.
- the outward path is labelled OUT and the return path, later in time, is labelled RTN.
- the robot is considerably more capable of steering without bumping into obstacles after the period 7900 - 8900 spend in the top left-hand corner. This is due to the amount of learning the control system has achieved during that period, as the robot has had to bump a large number of obstacles to be able to steer out of the corner.
- the sensors used to effect environmental sensing could equally well be provided using different sensor technologies, such as ultrasonic range sensors, image processing visual sensors, radiation sensors, electromagnetic field sensors, radar sensors etc, the method by which the robot senses its environment not being essential to the novel invention.
- the method by which the CMP filter-based robot achieves optimised weights associated with each disturbance is not restricted to a “learning” process.
- the “learning” may have been achieved by another robot and the “learnt” parameters passed over as a starting condition to an “unlearnt” robot, such that the “unlearnt” robot can immediately negotiate a “maze” of obstacles.
- the CMP-based filter robot may be capable of further adapting the weights associated with each disturbance as time progresses to allow the robot to adapt to changes such as a different environment or physical degradation, or may employ fixed weights as a lower cost solution, at the expense of loss of adaptability to changing environments or physical degradation of the robot.
Landscapes
- Engineering & Computer Science (AREA)
- Artificial Intelligence (AREA)
- Health & Medical Sciences (AREA)
- Computer Vision & Pattern Recognition (AREA)
- Evolutionary Computation (AREA)
- Medical Informatics (AREA)
- Software Systems (AREA)
- Physics & Mathematics (AREA)
- General Physics & Mathematics (AREA)
- Automation & Control Theory (AREA)
- Feedback Control In General (AREA)
Abstract
Description
-
- receiving a primary input signal representing a measured state of the apparatus,
- generating a control signal for influencing the state of the apparatus in response to said primary input signal so as to maintain a desired state; and
- receiving at least one further input for signal representing additional measurements of the apparatus or its environment,
- including corrections in said control signal in response to said additional measurement signal, and
- conditioning the response of said correcting means automatically in response to temporal cross-correlation observed between said additional measurement signal and said control signal observed during operation of the controller and apparatus together.
where u is given by:
u 1(t)=z 1(t) h 1(t) (2)
where x is convolved with h. functions h are the transfer functions of
where H(s) describes the resonator in Laplace notation as usual with the two complex/complex-conjugate parameters p and p* given by p=a+ib and p*=a−ib with:
where f is the resonant frequency of the relevant resonators 611-615 and Q is their damping factor. (The value of Q is approximately identical to the number of oscillations a resonator will make in response to a δ-function input.) For the purpose of this application Q would preferably be approximately 1, for example lying in the range 0.5-1.2. As discussed earlier, the frequency response depends upon the reaction time required of the controller in a real application. If a CMP filter is used within an electronic control loop, f can be very high (kilohertz to megahertz), if used in a mechanical system f will normally be in the 1-100 hertz range, if used in chemical control situations f can be in the range of millihertz or even lower.
ρi→ρi+Δρi (5a)
Δρi(t)=μui(t)v′(t) (5b)
where μ is a small number typically in the range of 0.000001 to 0.1, which is a damping factor applied to all variable gain blocks 621-625 to prevent too rapid gain changes, and v′(t) is the temporal derivative of v(t) computed by the
Claims (41)
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US11/513,681 US7558634B2 (en) | 2001-06-05 | 2006-08-30 | Controller and method of controlling an apparatus using predictive filters |
US12/473,178 US8032237B2 (en) | 2001-06-05 | 2009-05-27 | Correction signal capable of diminishing a future change to an output signal |
Applications Claiming Priority (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB0113627.4 | 2001-06-05 | ||
GBGB0113627.4A GB0113627D0 (en) | 2001-06-05 | 2001-06-05 | Controller and method of controlling an apparatus |
PCT/GB2002/002571 WO2002099544A1 (en) | 2001-06-05 | 2002-06-05 | Controller and method of controlling an apparatus |
US10/479,741 US7107108B2 (en) | 2001-06-05 | 2002-06-05 | Controller and method of controlling an apparatus using predictive filters |
US11/513,681 US7558634B2 (en) | 2001-06-05 | 2006-08-30 | Controller and method of controlling an apparatus using predictive filters |
Related Parent Applications (3)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/GB2002/002571 Continuation WO2002099544A1 (en) | 2001-06-05 | 2002-06-05 | Controller and method of controlling an apparatus |
US10/479,741 Continuation US7107108B2 (en) | 2001-06-05 | 2002-06-05 | Controller and method of controlling an apparatus using predictive filters |
US10479741 Continuation | 2002-06-05 |
Related Child Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US12/473,178 Continuation US8032237B2 (en) | 2001-06-05 | 2009-05-27 | Correction signal capable of diminishing a future change to an output signal |
Publications (2)
Publication Number | Publication Date |
---|---|
US20080091282A1 US20080091282A1 (en) | 2008-04-17 |
US7558634B2 true US7558634B2 (en) | 2009-07-07 |
Family
ID=9915930
Family Applications (3)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US10/479,741 Expired - Lifetime US7107108B2 (en) | 2001-06-05 | 2002-06-05 | Controller and method of controlling an apparatus using predictive filters |
US11/513,681 Expired - Lifetime US7558634B2 (en) | 2001-06-05 | 2006-08-30 | Controller and method of controlling an apparatus using predictive filters |
US12/473,178 Expired - Fee Related US8032237B2 (en) | 2001-06-05 | 2009-05-27 | Correction signal capable of diminishing a future change to an output signal |
Family Applications Before (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US10/479,741 Expired - Lifetime US7107108B2 (en) | 2001-06-05 | 2002-06-05 | Controller and method of controlling an apparatus using predictive filters |
Family Applications After (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US12/473,178 Expired - Fee Related US8032237B2 (en) | 2001-06-05 | 2009-05-27 | Correction signal capable of diminishing a future change to an output signal |
Country Status (5)
Country | Link |
---|---|
US (3) | US7107108B2 (en) |
EP (3) | EP1780618A1 (en) |
DE (2) | DE60236035D1 (en) |
GB (1) | GB0113627D0 (en) |
WO (1) | WO2002099544A1 (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8032237B2 (en) | 2001-06-05 | 2011-10-04 | Elverson Hopewell Llc | Correction signal capable of diminishing a future change to an output signal |
US9889566B2 (en) | 2015-05-01 | 2018-02-13 | General Electric Company | Systems and methods for control of robotic manipulation |
US10471595B2 (en) | 2016-05-31 | 2019-11-12 | Ge Global Sourcing Llc | Systems and methods for control of robotic manipulation |
Families Citing this family (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6996442B2 (en) * | 2003-01-15 | 2006-02-07 | Xerox Corporation | Systems and methods for detecting impending faults within closed-loop control systems |
DE10342769A1 (en) * | 2003-09-16 | 2005-04-21 | Voith Paper Patent Gmbh | System for computer-aided measurement of quality and / or process data |
US7481763B2 (en) * | 2004-05-28 | 2009-01-27 | Ethicon Endo-Surgery, Inc. | Metal bellows position feedback for hydraulic control of an adjustable gastric band |
US7603186B2 (en) * | 2006-04-28 | 2009-10-13 | Advanced Energy Industries, Inc. | Adaptive response time closed loop control algorithm |
US7930639B2 (en) | 2007-09-26 | 2011-04-19 | Rockwell Automation Technologies, Inc. | Contextualization for historians in industrial systems |
WO2009076968A2 (en) | 2007-12-19 | 2009-06-25 | Vestas Wind Systems A/S | Event-based control system for wind turbine generators |
NL2007606A (en) * | 2010-11-22 | 2012-05-23 | Asml Netherlands Bv | Controller, lithographic apparatus, method of controlling the position of an object and device manufacturing method. |
JP6536978B1 (en) * | 2018-03-15 | 2019-07-03 | オムロン株式会社 | Learning device, learning method, and program thereof |
CN115291507B (en) * | 2022-01-06 | 2023-05-26 | 兰州理工大学 | Mine filling slurry concentration sliding mode control method and system |
DE102022132996B3 (en) | 2022-12-12 | 2024-05-08 | Georg-August-Universität Göttingen Stiftung Öffentlichen Rechts | Method and device for determining a time offset between signals at different signal inputs |
Citations (53)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3013721A (en) | 1959-08-18 | 1961-12-19 | Industrial Nucleonics Corp | Automatic control system |
US3862403A (en) | 1973-04-20 | 1975-01-21 | Hitachi Ltd | Plant optimizing control device |
US4389618A (en) | 1981-04-15 | 1983-06-21 | The United States Of America As Represented By The Secretary Of The Navy | Adaptive feed-forward system |
JPS58165106A (en) | 1982-03-26 | 1983-09-30 | Toshiba Corp | Feedforward controller |
US4518866A (en) | 1982-09-28 | 1985-05-21 | Psychologics, Inc. | Method of and circuit for simulating neurons |
US4634946A (en) | 1985-10-02 | 1987-01-06 | Westinghouse Electric Corp. | Apparatus and method for predictive control of a dynamic system |
US4663703A (en) | 1985-10-02 | 1987-05-05 | Westinghouse Electric Corp. | Predictive model reference adaptive controller |
US4698745A (en) | 1984-02-07 | 1987-10-06 | Kabushiki Kaisha Toshiba | Process control apparatus for optimal adaptation to a disturbance |
US4714988A (en) | 1982-03-26 | 1987-12-22 | Kabushiki Kaisha Toshiba | Feedforward feedback control having predictive disturbance compensation |
US4809330A (en) * | 1984-04-23 | 1989-02-28 | Nec Corporation | Encoder capable of removing interaction between adjacent frames |
EP0334698A2 (en) | 1988-03-23 | 1989-09-27 | Measurex Corporation | Dead time compensated control loop |
US5146414A (en) * | 1990-04-18 | 1992-09-08 | Interflo Medical, Inc. | Method and apparatus for continuously measuring volumetric flow |
US5159660A (en) | 1990-08-09 | 1992-10-27 | Western Thunder | Universal process control using artificial neural networks |
US5235646A (en) * | 1990-06-15 | 1993-08-10 | Wilde Martin D | Method and apparatus for creating de-correlated audio output signals and audio recordings made thereby |
US5311421A (en) | 1989-12-08 | 1994-05-10 | Hitachi, Ltd. | Process control method and system for performing control of a controlled system by use of a neural network |
DE4340746A1 (en) | 1992-11-30 | 1994-06-01 | Toyota Chuo Kenkyusho Aichi Kk | Dynamic system error diagnostic appts., e.g. for motor vehicle - determines integrated disturbance vector, consisting of sum of external and internal vectors of dynamic system, based on internal state vector of dynamic system, and cross-correlates with internal state vector |
US5404289A (en) | 1993-08-30 | 1995-04-04 | National University Of Singapore | Controller apparatus having improved transient response speed by means of self-tuning variable set point weighting |
US5490505A (en) | 1991-03-07 | 1996-02-13 | Masimo Corporation | Signal processing apparatus |
US5513098A (en) | 1993-06-04 | 1996-04-30 | The Johns Hopkins University | Method for model-free control of general discrete-time systems |
US5517418A (en) | 1993-04-26 | 1996-05-14 | Hughes Aircraft Company | Spacecraft disturbance compensation using feedforward control |
US5519605A (en) | 1994-10-24 | 1996-05-21 | Olin Corporation | Model predictive control apparatus and method |
US5521946A (en) | 1994-01-07 | 1996-05-28 | The 3Do Company | Multi-phase filter/DAC |
US5570282A (en) | 1994-11-01 | 1996-10-29 | The Foxboro Company | Multivariable nonlinear process controller |
US5704011A (en) | 1994-11-01 | 1997-12-30 | The Foxboro Company | Method and apparatus for providing multivariable nonlinear control |
US5710500A (en) | 1994-04-28 | 1998-01-20 | Matsushita Electric Industrial Co., Ltd. | Motor speed control apparatus using phase-advance based estimated disturbance signal |
US5719788A (en) * | 1995-04-18 | 1998-02-17 | The Regents Of The University Of California | Automatic detection of excessively oscillatory feedback control loops. |
US5761918A (en) * | 1995-05-01 | 1998-06-09 | Index Sensors And Controls, Inc. | Integrated controller for commercial vehicle air conditioning system |
US5822740A (en) | 1996-06-28 | 1998-10-13 | Honeywell Inc. | Adaptive fuzzy controller that modifies membership functions |
US5893055A (en) * | 1997-05-30 | 1999-04-06 | Abb Industrial Systems, Inc. | Two-dimensional web property variation modeling and control |
US6055524A (en) | 1997-10-06 | 2000-04-25 | General Cybernation Group, Inc. | Model-free adaptive process control |
US6064916A (en) * | 1997-04-29 | 2000-05-16 | Sunkyung Engineering & Construction Limited | Hybrid predictor, hybrid prediction method, and system for and method of controlling processes using the hybrid predictor and hybrid preedition method |
US6064997A (en) | 1997-03-19 | 2000-05-16 | University Of Texas System, The Board Of Regents | Discrete-time tuning of neural network controllers for nonlinear dynamical systems |
US6094602A (en) | 1996-11-29 | 2000-07-25 | Woodward Governor Company | Method and apparatus for estimating and controlling non-linear disturbances in a feedback control system |
EP1030231A1 (en) | 1999-02-19 | 2000-08-23 | Neles Field Controls Oy | A method of tuning a process control loop in an industrial process. |
US6125124A (en) | 1996-09-16 | 2000-09-26 | Nokia Technology Gmbh | Synchronization and sampling frequency in an apparatus receiving OFDM modulated transmissions |
US6182001B1 (en) * | 1996-12-25 | 2001-01-30 | Kabushiki Kaisha Toyota Chuo Kenkyusho | Braking estimation device, anti-lock brake controller, and braking pressure controller |
US6181975B1 (en) | 1996-06-19 | 2001-01-30 | Arch Development Corporation | Industrial process surveillance system |
US6185309B1 (en) | 1997-07-11 | 2001-02-06 | The Regents Of The University Of California | Method and apparatus for blind separation of mixed and convolved sources |
WO2001035175A1 (en) | 1999-11-10 | 2001-05-17 | Adaptive Control Limited | Controllers for multichannel feedforward control of stochastic disturbances |
US6314127B1 (en) * | 1999-02-23 | 2001-11-06 | Lucent Technologies Inc. | System and method for enhancing signal reception |
EP1179671A2 (en) | 2000-08-07 | 2002-02-13 | Volkswagen Aktiengesellschaft | Method for checking a fuel injection system |
US6445963B1 (en) | 1999-10-04 | 2002-09-03 | Fisher Rosemount Systems, Inc. | Integrated advanced control blocks in process control systems |
WO2002099544A1 (en) | 2001-06-05 | 2002-12-12 | University Of Stirling | Controller and method of controlling an apparatus |
US20020191711A1 (en) | 2000-03-10 | 2002-12-19 | Martin Weiss | Method of determining parameters of an n-gate |
US6577908B1 (en) | 2000-06-20 | 2003-06-10 | Fisher Rosemount Systems, Inc | Adaptive feedback/feedforward PID controller |
US6594605B2 (en) * | 2000-02-03 | 2003-07-15 | Advantest Corp. | Correlation function measuring method and apparatus |
US6611319B2 (en) * | 2000-05-19 | 2003-08-26 | Optical Scientific, Inc. | Optical flow sensor using a fast correlation algorithm |
US6658304B1 (en) | 1999-05-10 | 2003-12-02 | Abb Ab | Computer based method and a system for controlling an industrial process |
US6754542B1 (en) | 1999-10-18 | 2004-06-22 | Yamatake Corporation | Control arithmetic apparatus and method |
US6772036B2 (en) | 2001-08-30 | 2004-08-03 | Fisher-Rosemount Systems, Inc. | Control system using process model |
US6937909B2 (en) | 2003-07-02 | 2005-08-30 | Johnson Controls Technology Company | Pattern recognition adaptive controller |
US6937910B2 (en) | 2000-11-15 | 2005-08-30 | Abb Ab | Method and a system for evaluating whether a signal is suitable for feed-forward control |
US6967988B1 (en) * | 1999-07-31 | 2005-11-22 | Alcatel | Filter for determining cross-correlation, receiver, and method of equalizing signals |
Family Cites Families (19)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
BE793564A (en) * | 1971-12-30 | 1973-04-16 | Western Electric Co | ANALOGUE-DIGITAL CONVERTER |
JPS60164805A (en) * | 1984-02-07 | 1985-08-27 | Toshiba Corp | Process controller |
JPH0653378B2 (en) * | 1986-05-24 | 1994-07-20 | 住友重機械工業株式会社 | Control method of injection molding machine |
US5541833A (en) * | 1987-03-30 | 1996-07-30 | The Foxboro Company | Multivariable feedforward adaptive controller |
JPH03118618A (en) * | 1989-09-30 | 1991-05-21 | Fanuc Ltd | Control system applying sliding mode control having damping effect |
JP2879946B2 (en) * | 1990-06-04 | 1999-04-05 | 帝人製機株式会社 | Aircraft wing flutter suppression system |
US5394322A (en) * | 1990-07-16 | 1995-02-28 | The Foxboro Company | Self-tuning controller that extracts process model characteristics |
GB9103777D0 (en) * | 1991-02-22 | 1991-04-10 | B & W Loudspeakers | Analogue and digital convertors |
JPH05134710A (en) * | 1991-07-18 | 1993-06-01 | Toshiba Corp | Neural network feed-forward control equipment |
JPH06274205A (en) * | 1993-03-22 | 1994-09-30 | Toshiba Corp | Gain adaptive control device |
US5883482A (en) * | 1993-07-08 | 1999-03-16 | The Gleason Works | Method and apparatus for controlling a drive in a machine tool |
US5710550A (en) | 1995-08-17 | 1998-01-20 | I-Cube, Inc. | Apparatus for programmable signal switching |
JPH09134203A (en) * | 1995-11-13 | 1997-05-20 | Mitsubishi Heavy Ind Ltd | Distribution controller |
KR100267364B1 (en) * | 1996-04-30 | 2000-10-16 | 윤종용 | Adaptive feed forward device for reducing current control error |
US5992383A (en) * | 1996-05-28 | 1999-11-30 | U.S. Philips Corporation | Control unit having a disturbance predictor, a system controlled by such a control unit, an electrical actuator controlled by such a control unit, and throttle device provided with such an actuator |
DE19629845A1 (en) * | 1996-07-24 | 1998-01-29 | Rexroth Mannesmann Gmbh | PID controller |
US5997778A (en) * | 1998-04-23 | 1999-12-07 | Van Dorn Demag Corporation | Auto-tuned, adaptive process controlled, injection molding machine |
JP3498894B2 (en) * | 1998-04-28 | 2004-02-23 | 株式会社日立製作所 | Control target identification method |
JP3552158B2 (en) * | 1999-04-08 | 2004-08-11 | 富士通株式会社 | Storage device |
-
2001
- 2001-06-05 GB GBGB0113627.4A patent/GB0113627D0/en not_active Ceased
-
2002
- 2002-06-05 EP EP07100309A patent/EP1780618A1/en not_active Withdrawn
- 2002-06-05 EP EP07100308A patent/EP1780617B1/en not_active Expired - Lifetime
- 2002-06-05 WO PCT/GB2002/002571 patent/WO2002099544A1/en active IP Right Grant
- 2002-06-05 DE DE60236035T patent/DE60236035D1/en not_active Expired - Lifetime
- 2002-06-05 DE DE60217487T patent/DE60217487T2/en not_active Expired - Lifetime
- 2002-06-05 EP EP02732912A patent/EP1397727B1/en not_active Expired - Lifetime
- 2002-06-05 US US10/479,741 patent/US7107108B2/en not_active Expired - Lifetime
-
2006
- 2006-08-30 US US11/513,681 patent/US7558634B2/en not_active Expired - Lifetime
-
2009
- 2009-05-27 US US12/473,178 patent/US8032237B2/en not_active Expired - Fee Related
Patent Citations (55)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3013721A (en) | 1959-08-18 | 1961-12-19 | Industrial Nucleonics Corp | Automatic control system |
US3862403A (en) | 1973-04-20 | 1975-01-21 | Hitachi Ltd | Plant optimizing control device |
US4389618A (en) | 1981-04-15 | 1983-06-21 | The United States Of America As Represented By The Secretary Of The Navy | Adaptive feed-forward system |
JPS58165106A (en) | 1982-03-26 | 1983-09-30 | Toshiba Corp | Feedforward controller |
US4714988A (en) | 1982-03-26 | 1987-12-22 | Kabushiki Kaisha Toshiba | Feedforward feedback control having predictive disturbance compensation |
US4518866A (en) | 1982-09-28 | 1985-05-21 | Psychologics, Inc. | Method of and circuit for simulating neurons |
US4698745A (en) | 1984-02-07 | 1987-10-06 | Kabushiki Kaisha Toshiba | Process control apparatus for optimal adaptation to a disturbance |
US4809330A (en) * | 1984-04-23 | 1989-02-28 | Nec Corporation | Encoder capable of removing interaction between adjacent frames |
US4663703A (en) | 1985-10-02 | 1987-05-05 | Westinghouse Electric Corp. | Predictive model reference adaptive controller |
US4634946A (en) | 1985-10-02 | 1987-01-06 | Westinghouse Electric Corp. | Apparatus and method for predictive control of a dynamic system |
EP0334698A2 (en) | 1988-03-23 | 1989-09-27 | Measurex Corporation | Dead time compensated control loop |
US5311421A (en) | 1989-12-08 | 1994-05-10 | Hitachi, Ltd. | Process control method and system for performing control of a controlled system by use of a neural network |
US5146414A (en) * | 1990-04-18 | 1992-09-08 | Interflo Medical, Inc. | Method and apparatus for continuously measuring volumetric flow |
US5235646A (en) * | 1990-06-15 | 1993-08-10 | Wilde Martin D | Method and apparatus for creating de-correlated audio output signals and audio recordings made thereby |
US5159660A (en) | 1990-08-09 | 1992-10-27 | Western Thunder | Universal process control using artificial neural networks |
US5490505A (en) | 1991-03-07 | 1996-02-13 | Masimo Corporation | Signal processing apparatus |
DE4340746A1 (en) | 1992-11-30 | 1994-06-01 | Toyota Chuo Kenkyusho Aichi Kk | Dynamic system error diagnostic appts., e.g. for motor vehicle - determines integrated disturbance vector, consisting of sum of external and internal vectors of dynamic system, based on internal state vector of dynamic system, and cross-correlates with internal state vector |
US5412584A (en) | 1992-11-30 | 1995-05-02 | Kabushiki Kaisha Toyota Chuo Kenkyusho | Dynamic system diagnosing apparatus, tire air pressure diagnosing apparatus and vehicle body weight change detecting apparatus using same |
US5517418A (en) | 1993-04-26 | 1996-05-14 | Hughes Aircraft Company | Spacecraft disturbance compensation using feedforward control |
US5513098A (en) | 1993-06-04 | 1996-04-30 | The Johns Hopkins University | Method for model-free control of general discrete-time systems |
US5404289A (en) | 1993-08-30 | 1995-04-04 | National University Of Singapore | Controller apparatus having improved transient response speed by means of self-tuning variable set point weighting |
US5521946A (en) | 1994-01-07 | 1996-05-28 | The 3Do Company | Multi-phase filter/DAC |
US5710500A (en) | 1994-04-28 | 1998-01-20 | Matsushita Electric Industrial Co., Ltd. | Motor speed control apparatus using phase-advance based estimated disturbance signal |
US5519605A (en) | 1994-10-24 | 1996-05-21 | Olin Corporation | Model predictive control apparatus and method |
US5570282A (en) | 1994-11-01 | 1996-10-29 | The Foxboro Company | Multivariable nonlinear process controller |
US5704011A (en) | 1994-11-01 | 1997-12-30 | The Foxboro Company | Method and apparatus for providing multivariable nonlinear control |
US5719788A (en) * | 1995-04-18 | 1998-02-17 | The Regents Of The University Of California | Automatic detection of excessively oscillatory feedback control loops. |
US5761918A (en) * | 1995-05-01 | 1998-06-09 | Index Sensors And Controls, Inc. | Integrated controller for commercial vehicle air conditioning system |
US6181975B1 (en) | 1996-06-19 | 2001-01-30 | Arch Development Corporation | Industrial process surveillance system |
US5822740A (en) | 1996-06-28 | 1998-10-13 | Honeywell Inc. | Adaptive fuzzy controller that modifies membership functions |
US6125124A (en) | 1996-09-16 | 2000-09-26 | Nokia Technology Gmbh | Synchronization and sampling frequency in an apparatus receiving OFDM modulated transmissions |
US6094602A (en) | 1996-11-29 | 2000-07-25 | Woodward Governor Company | Method and apparatus for estimating and controlling non-linear disturbances in a feedback control system |
US6182001B1 (en) * | 1996-12-25 | 2001-01-30 | Kabushiki Kaisha Toyota Chuo Kenkyusho | Braking estimation device, anti-lock brake controller, and braking pressure controller |
US6064997A (en) | 1997-03-19 | 2000-05-16 | University Of Texas System, The Board Of Regents | Discrete-time tuning of neural network controllers for nonlinear dynamical systems |
US6064916A (en) * | 1997-04-29 | 2000-05-16 | Sunkyung Engineering & Construction Limited | Hybrid predictor, hybrid prediction method, and system for and method of controlling processes using the hybrid predictor and hybrid preedition method |
US5893055A (en) * | 1997-05-30 | 1999-04-06 | Abb Industrial Systems, Inc. | Two-dimensional web property variation modeling and control |
US6185309B1 (en) | 1997-07-11 | 2001-02-06 | The Regents Of The University Of California | Method and apparatus for blind separation of mixed and convolved sources |
US6055524A (en) | 1997-10-06 | 2000-04-25 | General Cybernation Group, Inc. | Model-free adaptive process control |
EP1030231A1 (en) | 1999-02-19 | 2000-08-23 | Neles Field Controls Oy | A method of tuning a process control loop in an industrial process. |
US6314127B1 (en) * | 1999-02-23 | 2001-11-06 | Lucent Technologies Inc. | System and method for enhancing signal reception |
US6658304B1 (en) | 1999-05-10 | 2003-12-02 | Abb Ab | Computer based method and a system for controlling an industrial process |
US6967988B1 (en) * | 1999-07-31 | 2005-11-22 | Alcatel | Filter for determining cross-correlation, receiver, and method of equalizing signals |
US6445963B1 (en) | 1999-10-04 | 2002-09-03 | Fisher Rosemount Systems, Inc. | Integrated advanced control blocks in process control systems |
US6754542B1 (en) | 1999-10-18 | 2004-06-22 | Yamatake Corporation | Control arithmetic apparatus and method |
WO2001035175A1 (en) | 1999-11-10 | 2001-05-17 | Adaptive Control Limited | Controllers for multichannel feedforward control of stochastic disturbances |
US6594605B2 (en) * | 2000-02-03 | 2003-07-15 | Advantest Corp. | Correlation function measuring method and apparatus |
US20020191711A1 (en) | 2000-03-10 | 2002-12-19 | Martin Weiss | Method of determining parameters of an n-gate |
US6611319B2 (en) * | 2000-05-19 | 2003-08-26 | Optical Scientific, Inc. | Optical flow sensor using a fast correlation algorithm |
US6577908B1 (en) | 2000-06-20 | 2003-06-10 | Fisher Rosemount Systems, Inc | Adaptive feedback/feedforward PID controller |
DE10038444A1 (en) | 2000-08-07 | 2002-02-21 | Volkswagen Ag | Testing fuel injection system involves cross-correlating sensor signal with control signal for actuator for influencing induction air pressure and evaluating cross-correlation coefficient |
EP1179671A2 (en) | 2000-08-07 | 2002-02-13 | Volkswagen Aktiengesellschaft | Method for checking a fuel injection system |
US6937910B2 (en) | 2000-11-15 | 2005-08-30 | Abb Ab | Method and a system for evaluating whether a signal is suitable for feed-forward control |
WO2002099544A1 (en) | 2001-06-05 | 2002-12-12 | University Of Stirling | Controller and method of controlling an apparatus |
US6772036B2 (en) | 2001-08-30 | 2004-08-03 | Fisher-Rosemount Systems, Inc. | Control system using process model |
US6937909B2 (en) | 2003-07-02 | 2005-08-30 | Johnson Controls Technology Company | Pattern recognition adaptive controller |
Non-Patent Citations (11)
Title |
---|
"International Search Report Based on EP Application No. 07100308.1". |
"International Search Report Based on EP Application No. 07100309.9", (May 2, 2007). |
"Notice of Allowability in related patent application no. 10/479,741", (Sep. 12, 2006). |
Bozic, "Digital and Kalman Filtering," published 1994 by Edward Arnold, Chapter 7, Recursive Estimation. |
Comments on Statement of Reasons for Allowance, filed with Issue Fee Jul. 20, 2006, in related U.S. Appl. No. 10/479,741, now Patent No. 7,107,108, issued Sep. 12, 2006. |
Elliott, "Optimal Controllers and Adaptive Controllers for Multichannel Feedforward Control of Stochastic Disturbances", IEEE Transactions on Signal Processing, vol. 48, No. 4, (Apr. 2000), 1053-1060. |
International Preliminary Examination Report based on Application No. PCT/GB 02/02571, University of Sterling, et al. |
International Search Report based on Application No. PCT/GB 02/02571, Sep. 24, 2002. |
Office Action mailed Oct. 13, 2005 in related U.S. Appl. No. 10/479,741, now Patent No. 7,107,108, issued Sep. 12, 2006. |
Preliminary Amendment filed in related U.S. Appl. No. 10/479,741, now Patent No. 7,107,108, issued Sep. 12, 2006. |
Response of Feb. 10, 2006 to Office Action mailed Oct. 13, 2005, in related U.S. Appl. No. 10/479,741, now Patent No. 7,107,108, issued Sep. 12, 2006. |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8032237B2 (en) | 2001-06-05 | 2011-10-04 | Elverson Hopewell Llc | Correction signal capable of diminishing a future change to an output signal |
US9889566B2 (en) | 2015-05-01 | 2018-02-13 | General Electric Company | Systems and methods for control of robotic manipulation |
US10252424B2 (en) | 2015-05-01 | 2019-04-09 | General Electric Company | Systems and methods for control of robotic manipulation |
US10471595B2 (en) | 2016-05-31 | 2019-11-12 | Ge Global Sourcing Llc | Systems and methods for control of robotic manipulation |
Also Published As
Publication number | Publication date |
---|---|
DE60217487D1 (en) | 2007-02-22 |
DE60217487T2 (en) | 2007-10-18 |
EP1780617A1 (en) | 2007-05-02 |
WO2002099544A1 (en) | 2002-12-12 |
EP1780617B1 (en) | 2010-04-14 |
EP1397727B1 (en) | 2007-01-10 |
GB0113627D0 (en) | 2001-07-25 |
US20090299499A1 (en) | 2009-12-03 |
US20050027373A1 (en) | 2005-02-03 |
US8032237B2 (en) | 2011-10-04 |
DE60236035D1 (en) | 2010-05-27 |
US20080091282A1 (en) | 2008-04-17 |
US7107108B2 (en) | 2006-09-12 |
EP1780618A1 (en) | 2007-05-02 |
EP1397727A1 (en) | 2004-03-17 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US7558634B2 (en) | Controller and method of controlling an apparatus using predictive filters | |
EP0710901B1 (en) | Multivariable nonlinear process controller | |
US5043863A (en) | Multivariable adaptive feedforward controller | |
EP0823078B1 (en) | Feedback method for controlling non-linear processes | |
Chen et al. | Applying neural networks to on-line updated PID controllers for nonlinear process control | |
US7805207B2 (en) | Method and apparatus for adaptive parallel proportional-integral-derivative controller | |
EP0710902B1 (en) | Method and apparatus for controlling multivariable nonlinear processes | |
WO1992007311A1 (en) | Universal process control using artificial neural networks | |
MXPA97008318A (en) | Feedback method for controlling non-linear processes | |
WO1999018483A1 (en) | Model-free adaptive process control | |
JPH01239603A (en) | Process controller | |
EP2105809A2 (en) | Method and apparatus for controlling system | |
CN101004591A (en) | Decoupling control method of non - square matrix system in industrial process | |
Lee et al. | Process/model mismatch compensation for model-based controllers | |
EP0307466B1 (en) | Multivariable adaptive feedforward controller | |
JPH09146610A (en) | Multivariable nonlinear process controller | |
US6959218B2 (en) | Partitioned control system and method | |
JPH07261805A (en) | Automatic adjusting device for proportional plus integral plus derivative control parameter | |
Grimble | Integral minimum variance control and benchmarking | |
RU2302028C1 (en) | Method for controlling dynamic objects | |
JPH0643904A (en) | Controlled variable adjusting device and motor controller | |
Lau et al. | Experimental evaluation of a Kalman filter based multistep adaptive predictive controller | |
Zhang et al. | Comparison of a nonlinear adaptive controller with certainty-equivalence type adaptive controllers | |
Ławryńczuk | Suboptimal nonlinear predictive control with MIMO neural Hammerstein models | |
JPH03265902A (en) | Process controller |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
STCF | Information on status: patent grant |
Free format text: PATENTED CASE |
|
FEPP | Fee payment procedure |
Free format text: PAYOR NUMBER ASSIGNED (ORIGINAL EVENT CODE: ASPN); ENTITY STATUS OF PATENT OWNER: LARGE ENTITY |
|
AS | Assignment |
Owner name: ELVERSON HOPEWELL LLC, CALIFORNIA Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:UNIVERSITY OF STERLING;REEL/FRAME:026692/0889 Effective date: 20041112 |
|
AS | Assignment |
Owner name: ELVERSON HOPEWELL LLC, CALIFORNIA Free format text: CORRECTIVE ASSIGNMENT TO CORRECT THE ASSIGNOR'S NAME PREVIOUSLY RECORDED ON REEL 026692 FRAME 0889. ASSIGNOR(S) HEREBY CONFIRMS THE ORIGINAL ASSIGNMENT;ASSIGNOR:UNIVERSITY OF STIRLING;REEL/FRAME:028074/0557 Effective date: 20041112 |
|
FPAY | Fee payment |
Year of fee payment: 4 |
|
AS | Assignment |
Owner name: ZARBANA DIGITAL FUND LLC, DELAWARE Free format text: MERGER;ASSIGNOR:ELVERSON HOPEWELL LLC;REEL/FRAME:037338/0731 Effective date: 20150811 |
|
FPAY | Fee payment |
Year of fee payment: 8 |
|
MAFP | Maintenance fee payment |
Free format text: PAYMENT OF MAINTENANCE FEE, 12TH YEAR, LARGE ENTITY (ORIGINAL EVENT CODE: M1553); ENTITY STATUS OF PATENT OWNER: LARGE ENTITY Year of fee payment: 12 |